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Manufacturing Nylon 66 from the Ground Up
Team USA Leif Burgess Kevin LaSalle Erin Tiedemann This is only a template. You may chose to use or not use this format. I highly recommend you use a format that works for your group. Class 4 estimation 85 million pounds annually Parameters of Interest Minimize Branching Controlled Viscosity Safety What is Nylon 66? Why Nylon 66? Objectives Process Flow Diagram and Material Balance Nylon 66 Safety and Other Considerations Highly exothermic reaction Block A Corrosion Economic Analysis Conclusions and Recommendations Our team would like to thank the entire Chemical Engineering Department for their guidance and assistance. We would also like to thank Kurtis from Eddy Pumps for providing pricing information. / Ammonia Toxic 20 g/hr Cyclopentanone Explosive 506 g/hr Sell price: 2.50$/kg DCFRR: 68% Replace Compressor Future Safety Analysis Block A Pump corrosion 3.13$/kg DCFRR: 192% NPT: yrs NPVi=10%: 101 MM$ This plant is a ‘GO’ Acknowledgments 2.50$/kg DCFRR: 68% NPT: 1.4 yrs NPVi=10%: 21 MM$ Bibliography
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